Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
101 words
A METHOD OF MANUFACTURING A SOLID ADSORBENT COMPRISING THE STEPS OF: A. CONTACTING A BASE MATERIAL COMPRISING X OR Y ZEOLITE WITH A FLUORIDE-CONTAINING AQUEOUS SOLUTION OF SODIUM HYDROXIDE AT FIRST ION EXCHANGE CONDITIONS TO EFFECT THE ADDITION OF SODIUM CATIONS TO AND THE EXTRACTION OF ALUMINA FROM SAID BASE MATERIAL; B. TREATING THE SODIUM-EXCHANGED BASE MATERIAL AT SECOND ION EXCHANGE CONDITIONS TO EFFECT THE ESSENTIALLY COMPLETE EXCHANGE OF SODIUM CATIONS WITH BARIUM OR BARIUM AND POTASSIUM CATIONS; AND, C. DRYING THE THUS EXCHANGED BASE MATERIAL AT CONDITIONS TO REDUCE THE LOI AT 900*C. TO LESS THAN ABOUT 10 WT. %.
Claim 2
Independent Claim
101 words
A METHOD OF MANUFACTURING A SOLID ADSORBENT COMPRISING THE STEPS OF: A. CONTACTING A BASE MATERIAL COMPRISING X OR Y ZEOLITE WITH A FLUORIDE-CONTAINING AQUEOUS SOLUTION OF SODIUM HYDROXIDE AT FIRST ION EXCHANGE CONDITIONS TO EFFECT THE ADDITION OF SODIUM CATIONS TO AND THE EXTRACTION OF ALUMINA FROM SAID BASE MATERIAL; B. TREATING THE SODIUM-EXCHANGED BASE MATERIAL AT SECOND ION EXCHANGE CONDITIONS TO EFFECT THE ESSENTIALLY COMPLETE EXCHANGE OF SODIUM CATIONS WITH BARIUM OR BARIUM AND POTASSIUM CATIONS; AND, C. DRYING THE THUS EXCHANGED BASE MATERIAL AT CONDITIONS TO REDUCE THE LOI AT 900*C. TO LESS THAN ABOUT 10 WT. %.
Claim 3
Dependent Claim
21 words
The method of claim 1 further characterized in that said base material has a Na2O/Al2O3 ratio of about 0.7 or less.
Claim 4
Dependent Claim
38 words
The method of claim 1 further characterized in that said solution contains sodium fluoride in a concentration of less than its solubility limit and sodium hydroxide in a concentration of from about 0.5 to about 10 wt. %.
Claim 5
Dependent Claim
29 words
The method of claim 1 further characterized in that said first ion exchange conditions include a temperature within the range of from about 50* F. to about 250* F.
Claim 6
Dependent Claim
22 words
The method of claim 1 further characterized in that said sodium exchanged base material has a Na2O/Al2O3 ratio greater than about 0.7.
Claim 7
Dependent Claim
43 words
The method of claim 1 further characterized in that said second ion exchange conditions include a pH sufficient to preculde formation of the hydrogen form of the zeolite, and a temperature within the range of fRom about 50* F. to about 250* F.
Claim 8
Dependent Claim
22 words
The method of claim 1 further characterized in that said sodium-exchanged base material is essentially completely exchanged with barium and potassium cations.
Claim 9
Dependent Claim
23 words
The method of claim 7 further characterized in that the weight ratio of barium over potassium cations is from about 1.5 to 200.
Claim 10
Dependent Claim
20 words
The method of claim 1 further characterized in that said sodium-exchanged base material is essentially completely exchanged with barium cations.
Claim 11
Independent Claim
153 words
A method of manufacturing a solid adsorbent which comprises the steps of: a. contacting a base material comprising a X or Y structured zeolite having a Na2O/Al2O3 ratio of about 0.7 or less with a fluoride-containing aqueous sodium hydroxide solution at first ion exchange conditions to increase the sodium cation content of said mass to a Na2O/Al2O3 ratio of greater than about 0.7 and extract less than about 5% of the alumina from said base material; b. treating the sodium-exchanged base material at second ion exchange conditions, including a pH sufficient to preclude the formation of the hydrogen form of the zeolite and a temperature within the range of from about 50*F. to about 250*F., to effect the essentially complete exchange of sodium cations with barium or barium and potassium cations; and, c. drying the thus re-exchanged base material at conditions sufficient to reduce the LOI at 900*C. to less than about 10wt.%.
Claim 12
Independent Claim
153 words
A method of manufacturing a solid adsorbent which comprises the steps of: a. contacting a base material comprising a X or Y structured zeolite having a Na2O/Al2O3 ratio of about 0.7 or less with a fluoride-containing aqueous sodium hydroxide solution at first ion exchange conditions to increase the sodium cation content of said mass to a Na2O/Al2O3 ratio of greater than about 0.7 and extract less than about 5% of the alumina from said base material; b. treating the sodium-exchanged base material at second ion exchange conditions, including a pH sufficient to preclude the formation of the hydrogen form of the zeolite and a temperature within the range of from about 50*F. to about 250*F., to effect the essentially complete exchange of sodium cations with barium or barium and potassium cations; and, c. drying the thus re-exchanged base material at conditions sufficient to reduce the LOI at 900*C. to less than about 10wt.%.
Claim 13
Dependent Claim
37 words
The method of claim 10 further characterized in that said solution contains sodium fluoride in a concentration less than its solubility limit and sodium hydroxide in a concentration of from about 0.5 to about 10 wt. %.
Claim 14
Dependent Claim
32 words
The method of claim 10 further characterized in that said sodium-exchanged base material is essentially completely exchanged with barium and potassium cations in a weight ratio of from about 1.5 to 200.
Claim 15
Dependent Claim
19 words
The method of claim 10 further characterized in that said sodium-exchanged base material is completely exchanged with barium cations.
Claim 16
Dependent Claim
93 words
A solid adsorbent prepared by contacting a base material comprising X or Y structured zeolite with a fluoride containing aqueous sodium hydroxide solution at first ion exchange conditions to effect the addition of sodium cations to and the extraction of alumina from said base material, treating the sodium-exchanged base material at second ion exchange conditions to effect the essentially complete exchange of sodium cations with barium or barium and potassium cations and drying the thus exchanged base material at conditions to reduce the LOI at 900*C. to less than about 10 wt. %.
Claim 17
Dependent Claim
93 words
A solid adsorbent prepared by contacting a base material comprising X or Y structured zeolite with a fluoride containing aqueous sodium hydroxide solution at first ion exchange conditions to effect the addition of sodium cations to and the extraction of alumina from said base material, treating the sodium-exchanged base material at second ion exchange conditions to effect the essentially complete exchange of sodium cations with barium or barium and potassium cations and drying the thus exchanged base material at conditions to reduce the LOI at 900*C. to less than about 10 wt. %.